WO2014183987A1

WO2014183987A1 - Superabsorbent polymers with rapid absorption properties and process for producing same

Info

Publication number: WO2014183987A1
Application number: PCT/EP2014/058661
Authority: WO
Inventors: Laurent Wattebled; Anna MIASNIKOVA; Markus Henn
Original assignee: Evonik Industries Ag
Priority date: 2013-05-15
Filing date: 2014-04-29
Publication date: 2014-11-20
Also published as: KR20160010516A; EP2997057A1; CN105377921A; BR112015028304B1; KR101786285B1; US11001692B2; TWI495669B; JP6314211B2; EP2997057B1; DE102013208942A1; JP2016524634A; CN105377921B; US20160096944A1; TW201443111A; BR112015028304A2

Abstract

The present invention relates to a process for producing a water-absorbing polymer, comprising the steps of (i) mixing (α1) from 0.1 to 99.999% by weight, preferably from 20 to 98.99% by weight and particularly preferably from 30 to 98.95% by weight, of polymerizable, ethylenically unsaturated monomers containing acid groups, or salts of said monomers, or polymerizable, ethylenically unsaturated monomers including a protonated or quaternized nitrogen, or a mixture of these, where preference is given to mixtures at least including ethylenically unsaturated monomers containing acid groups, preferably acrylic acid, (α2) from 0 to 70% by weight, preferably from 1 to 60% by weight and particularly preferably from 1 to 40% by weight, of polymerized, ethylenically unsaturated monomers copolymerizable with (α1), (α3) from 0.001 to 10% by weight, preferably from 0.01 to 7% by weight and particularly preferably from 0.05 to 5% by weight, of one or more crosslinking agents, (α4) from 0 to 30% by weight, preferably from 1 to 20% by weight and particularly preferably from 5 to 10% by weight, of water-soluble polymers, and (α5) from 0 to 20% by weight, preferably from 0.01 to 7% by weight and particularly preferably from 0.05 to 5% by weight, of one or more auxiliaries, where the total of the quantities by weight of (α1) to (α5) is 100% by weight, (ii) free-radical polymerization with crosslinking, in order to form a water-insoluble, aqueous untreated hydrogel polymer, (iii) drying of the hydrogel polymer, (iv) grinding and isolation by sieving of the water-absorbing polymer, (v) surface post-crosslinking of the ground and sieved hydrogel polymer and (vi) drying and finishing of the water-absorbing polymer, where the following are added to the aqueous monomer solution: before the addition of the initiator and the start of the free-radical polymerization from 0.01 to 5% by weight, preferably from 0.02 to 2% by weight and particularly preferably from 0.07 to 1% by weight, of at least one surfactant from the group of the non-ionic unsaturated polyether copolymers, and optionally from 0.01 to 5% by weight, preferably from 0.02 to 2% by weight and particularly preferably from 0.07 to 1% by weight, of a blowing agent with particle size from 10 μm to 900 μm, based on the water-absorbing polymer, a process for producing a hydrogel polymer, the product of the process, and the use.

Description

Superabsorbent polymers with fast absorption properties as well

Process for its preparation

The present invention relates to superabsorbent polymers having fast absorption properties and to processes for their preparation.

The current trend in diaper construction is to produce even thinner structures with reduced cellulose fiber content and increased superabsorbent content. The advantage of thinner constructions is not only improved comfort, but also reduced packaging and warehousing costs. With the trend towards ever thinner diaper constructions, the requirement profile for superabsorbents has changed significantly. Critically important now is the ability of the hydrogel to carry and distribute liquids. Due to the higher load of the hygiene article (amount of superabsorbent per unit area), the polymer must not form a barrier layer for subsequent liquid in the swollen state (gel blocking). If the product has good transport properties, optimum utilization of the entire hygiene article can be guaranteed. In addition to the permeability of the superabsorbents (SAP) (indicated in the form of the so-called "Saline Flow Conductivity - SFC") and the absorbency under a compressive load, the absorption rate of the superabsorbent particles (stated in amount of absorbed liquid per gram of superabsorbent per second) is particularly important Criterion, which makes it possible to determine whether an absorbent core containing this superabsorber in high concentration, which has only a low proportion of fluff, is able to absorb it quickly on its first contact with liquids (so-called "acquisition"). Among other things, this "acquisition" is dependent on the absorption rate of the superabsorbent material in the case of absorbent cores having a high superabsorber content.

Different protective rights are known from the prior art which should allow an increase in the absorption rate of superabsorbent particles. From the W096 / 17884A1 is a water-absorbing resin known in the monomer solution, a solid blowing agent having a particle diameter of 1 to 100 μηι is used. In principle, preference is given to organic azo compounds and in particular to acrylic acid salts of azo compounds containing an amino group. Pure carbonates, ammonium nitride or mixtures thereof may optionally be used.

The disadvantage here is the rapid conversion of the azo compounds as well as the basic dispersing of the small solid particles in the monomer solution. Larger particles can not be dispersed well without separation of particles and monomer solution in the dispersion before the gel point.

A disadvantage here is the use of superabsorbents, which are known from the prior art, that leakage problems occur because the SAP either absorbs the liquid too slowly and / or has an inappropriate liquid transport.

The current trend, especially in diaper construction, is to produce even thinner absorbent cores with reduced cellulose fiber content and increased superabsorber content. The advantage of thinner constructions is not only improved comfort, but also reduced packaging and warehousing costs. The latest generation of absorbent cores disclosed, for example, in WO-A-2008/155722, WO-A-2008/15571 1, WO-A-2008/155710, WO-A-2008/155702, WO-A-2008 / No. 155701, WO-A-2008/155699, EP-A-1 225 857, WO-A-01/15647, WO-A-201 1/120504, DE-A-10 2009 049 450, WO-A-2008 / 1 17109, WO-A-97/1 1659, EP-A-0 826 349, WO-A-98/37846, WO-A-95/1 1653, WO-A-95/1 1651, WO-A- 95/1 1652, WO-A-95/1 1654, WO-A-2004/071363 or WO-A-01/89439 is essentially cellulose-free (for which reason corresponding diapers are also referred to as "fluffless diaper" The immobilization of the superabsorbent particles, which takes place in cellulose-containing absorbent cores by the cellulose fibers, can be realized in this latest generation of absorbent cores by, for example, immobilizing the superabsorbent particles on a substrate surface by means of thermoplastic fibers.

With the trend towards ever thinner diaper constructions and the elimination of the temporary liquid storage and transfer function of the cellulose fibers, the requirement profile for superabsorbents has changed significantly. Critically important now is the ability of the hydrogel to prevent the leakage of urine directly at the time of micturition. This is due to the property of the superabsorbent / hydrogel achieved to effectively absorb the fluid during swelling and distribute it in the gel layer, while minimizing the amount of unbound urine in the diaper. Advantageous superabsorbents, due to their good transport properties, also lead to optimum utilization of the entire hygiene article.

From US 5,154,713 water-absorbing polymers are known which are prepared by means of a carbonate blowing agent in the monomer solution. Here, the introduction of the carbonate in the monomer significantly before the actual polymerization, and the addition of initiator from 5 to 15 minutes after dispersing the carbonate blowing agent, whereby a uniform distribution of these carbonate particles is no longer guaranteed and a significant part of the carbonate, if necessary already is discharged again. EP 0 644 207 discloses superabsorbent polymers which are likewise mixed with an organic carbonate blowing agent in the monomer solution. The disadvantage here is the use of amine compounds as well as the whereabouts of the cleavage products of the organic carbonates in the superabsorbent.

WO 2010/095427 discloses water-absorbing polymers in which a gas is dispersed in the monomer solution. This is nitrogen, argon, helium, carbon dioxide or similar, which should ensure a more porous structure. These microbubbles should be kept in the monomer solution by means of polyoxyethylene (20) sorbitan monostearate until polymerization commences. The disadvantage here is that the surfactants can be washed out of the final product again and adversely affect the performance. Critically important now is the ability of the hydrogel to prevent the leakage of urine directly at the time of micturition. This is achieved by the property of the superabsorbent / hydrogel to effectively pick up the liquid during swelling and distribute it in the gel layer while minimizing the amount of unbound urine in the diaper. Advantageous superabsorbents, due to their good transport properties, also lead to optimum utilization of the entire hygiene article.

The term "rewet" generally refers to the property of a superabsorbent or a composite containing a superabsorbent, which is capable of transferring liquid under pressure to an absorbent layer. Paper, filter paper, collagen, sponges. Foams or similar understood. From EP1858998B1 superabsorbent foams are known in which the monomer solution only under elevated pressure of 12 bar by the addition of carbon dioxide and surfactants gives a foam.

However, the superabsorbents known hitherto from the prior art are only insufficiently suitable for use in the new generation of cellulose-free diaper constructions described above.

In general, the present invention is based on the object to overcome the disadvantages resulting from the prior art.

In particular, it is the object of the present invention to provide a process for the preparation of a water-absorbing polymer which has an improved swelling rate and faster uptake of liquids while retaining the overall quality and in particular a high permeability.

In addition, it is a further object to carry out the process in an economically simple manner, wherein the use of organic additives is minimized, as well as a non-pressurized operation is to be ensured. In particular, it is an object of the present invention to provide a method by which water-absorbing polymers can be produced, wherein a particularly high swelling rate can be ensured.

In addition, a further object of the present invention is to provide a process by which water-absorbing polymers can be prepared which provide rapid and active liquid transport, e.g. ensure in thin diapers, so that fast absorption and good distribution, d. H. a corresponding capillarity is ensured. Another object of the invention is primarily to provide a water-absorbing polymer, composites containing such water-absorbing polymers, and chemical products containing such water-absorbing polymers or composites, wherein the water-absorbing polymers have a He he increased absorption rate for aqueous solutions.

These objects are achieved by the subject matter of the categorizing claims. Advantageous embodiments and developments that occur individually or in combination may be the subject of the respective dependent claims.

A contribution to the solution of the problem mentioned at the outset is provided by the process for the preparation of a water-absorbing polymer comprising the process steps

(i) mixing

(a1) 0.1 to 99.999% by weight, preferably 20 to 98.99% by weight and particularly preferably 30 to 98.95% by weight of polymerizable, ethylenically unsaturated, acid group-containing monomers or their salts or polymerisable, ethylenically unsaturated , a protonated or quaternized nitrogen-containing monomers, or mixtures thereof, wherein at least ethylenically unsaturated, acid group-containing monomers, preferably acrylic acid-containing mixtures are particularly preferred,

(a2) 0 to 70 wt .-%, preferably 1 to 60 wt .-% and particularly preferably 1 to 40 wt .-% of polymerizable, ethylenically unsaturated, with (a1) copolymerizable monomers,

(a3) 0.001 to 10 wt .-%, preferably 0.01 to 7 wt .-% and particularly preferably 0.05 to 5 wt .-% of one or more crosslinkers,

(a4) 0 to 30 wt .-%, preferably 1 to 20 wt .-% and particularly preferably 5 to 10 wt .-% of water-soluble polymers,

(a5) 0 to 20 wt .-%, preferably 0.01 to 7 wt .-% and particularly preferably 0.05 to

5% by weight of one or more auxiliary substances, the sum of the amounts by weight (a1) to (a5) being 100% by weight,

(ii) radical polymerization with crosslinking to give a water-insoluble,

to form aqueous untreated hydrogel polymer,

(iii) drying the hydrogel polymer,

(iv) grinding and screening the hydrogel polymer,

(V) surface postcrosslinking of the ground and sieved hydrogel polymer and

(vi) drying and packaging the water-absorbing polymer,

in which

the aqueous monomer solution, before the addition of the initiator and the start of the radical polymerization, 0.01 to 5 wt .-%, preferably 0.02 to 2 wt .-% and particularly preferably 0.07 to 1 wt .-% of at least one Surfactants from the group of nonionic unsaturated polyether copolymers and optionally 0.01 to 5 wt .-%, preferably 0.02 to 2 wt.% And particularly preferably 0.07 to 1 wt .-% of a blowing agent having a particle size of 10 μηη be added to 900μηι, based on the water-absorbing polymer. The term "water-absorbing polymer" is understood according to the invention as the superabsorber.

Another embodiment relates to the process for producing a water-absorbing hydrogel comprising the process steps

(i) mixing

(ii) radical polymerization with crosslinking to give a water-insoluble,

to form aqueous untreated hydrogel polymer,

(iii) drying the hydrogel polymer,

(iv) grinding and screening the hydrogel polymer,

in which

the aqueous monomer solution, before the addition of the initiator and the start of the radical polymerization, 0.01 to 5 wt .-%, preferably 0.02 to 2 wt .-% and particularly preferably 0.07 to 1 wt .-% of at least one Surfactants from the group of nonionic unsaturated polyether copolymers and optionally 0.01 to 5 wt .-%, preferably 0.02 to 2 wt.% And particularly preferably 0.07 to 1 wt .-% of a blowing agent having a particle size of 10 μηη be added to 900μηι, based on the hydrogel polymer. This hydrogel polymer according to the invention can be converted by means of a thermally induced post-crosslinking into a water-absorbing polymer (superabsorber) according to the invention

It is preferably ensured according to the invention that the surfactants are polymerized into the polymer network. Advantageously, this greatly reduces the amount of extractable surfactant constituents and minimally reduces the surface tension accordingly.

According to the invention, a finely porous gel structure is obtained by the addition of surfactants and blowing agent to the monomer solution after polymerization, and superabsorbent powders having a larger surface area are obtained. Advantageously, the inventive enlargement of the entire surface ensures faster absorption of the liquid compared to conventional SAPs. This is represented by the so-called FSR value. The water-absorbing polymers according to the invention have an FSR in the range from 0.30 to 0.70, preferably from 0.35 to 0.60, particularly preferably from 0.40 to 0.50.

According to the invention, the surface tension, in spite of the use of the surfactants, is in the range from above 50 mN / m, preferably above 55 mN / m, more preferably above 60 mN / m and most preferably above 65 mN / m. The surface tension is not greater than 71 mN / m according to the invention.

According to the invention, the permeability, referred to as SFC value (in the present invention always based on 1.5 g), of the water-absorbing polymer composition is in the range from 30 to 200, preferably 50 to 180 and particularly preferably in the range from 70 to 150.

The particle distribution PSD of the hydrogel polymer is designed according to the invention such that more than 60% by weight of the particles are in the range of 300 μm to 600 μm and less than 5% by weight of the particles are smaller than 150 μm.

With a low surface tension, this generally leads to increased "Rewet" values, eg backsheet rewet or leakage for the diaper in which such superabsorbents are used.This problem is advantageously prevented by the process according to the invention and in the form of the copolymerizable surfactants. The superabsorbents show good performance in terms of retention (CRC) and absorption against pressure (AAP). Tailor-made surfactants are added to the monomer solution for the preparation of the superabsorbents according to the invention. These specific surfactants contain functional groups that are polymerizable. According to the invention, these are unsaturated polyether copolymers which are composed of rather hydrophilic ethylene glycol units and rather hydrophobic alkylene glycol units having 3 to 6 C atoms. The unsaturated polyethers may contain one or more different alkylene glycol units in combination with ethylene glycol units. Preference is given to propylene glycol (for example 1, 2 or 1, 3-propanediol), butylene glycol (eg 1, 2, 1, 3 or 1, 4-butanediol), pentylene glycol (eg 1, 5-pentanediol, 1, 2 Pentanediol, 1,3-pentanediol, 1,4-pentanediol, 2,3-pentanediol, 2,4-pentanediol or 2,5-pentanediol) or hexylene glycol (eg 1,6-hexanediol). The alkylene glycol units may be random, block or gradient distributed in the surfactant. In the context of the present invention, the individual alkylene glycol units may be isotactic, syndiotactic or atactic sequences of the configuration in the molecule.

The degree of polymerization of the polyether structure of the surfactant is generally in the range from 2 to 100, preferably in the range from 4 to 50, particularly preferably in the range from 6 to 20. The stated degrees of alkoxylation in each case relate to the average degree of alkoxylation. Of course, production reasons are generally mixtures in which additional lower and higher oligomers may be included.

The unsaturated group may be a vinyl ether, (meth) allyl ether, 4-vinylbenzyl ether, (meth) acrylamide, methacrylic ester or acrylic ester group and is preferably at the chain end.

Also suitable as polymerisable surfactants are esters of polyether copolymers and ethacrylic acid, α-chloroacrylic acid, α-cyanoacrylic acid, β-methylacrylic acid (crotonic acid), α-phenylacrylic acid, β-acryloyloxypropionic acid, sorbic acid, α-chlorosorbic acid, 2'-methylisocrotonic acid, cinnamic acid, p-chlorocinnamic acid, ß-stearylic acid, itaconic acid, citraconic acid, mesaconic acid, glutaconic acid, aconitic acid, maleic acid, fumaric acid, tricarboxyethylene and maleic anhydride can be used.

In addition, esters of polyether copolymers and allylsulfonic acid or aliphatic or aromatic vinylsulfonic acids or acrylic or methacrylic sulfonic acids can be used, examples of aliphatic or aromatic vinylsulfonic acids being vinylsulfonic acid, 4-vinylbenzenylsulfonic acid, vinyltoluenesulfonic acid or styrenesulfonic acid, acrylic or methacrylic sulfonic acids from the group of. Sulfoethyl (meth) acrylate, sulfopropyl (meth) acrylate, 2-hydroxy-3-methacryloxypropyl pylsulfonic acid, (meth) acrylamido-alkylsulfonic acids from the group of 2-acrylamido-2-methylpropanesulfonic acid, phosphonic acid monomers from the group of the vinylphosphonic acid, allylphosphonic acid, vinylbenzylphosphonic acid,

(Meth) acrylamidoalkylphosphonic acids, acrylamidoalkyldiphosphonic acids, phonomonomethylated vinylamines and (meth) acrylicphosphonic acid derivatives, or acrylamides and methacrylamides from the group of alkyl-substituted (meth) acrylamides or aminoalkyl-substituted derivatives of the (meth) acrylamide from the group of N-methylol (meth) acrylamide vinylamides from the group of N-vinylamide, N-vinylformamide, N-vinylacetamide, N-vinyl-N-methylacetamide, N-vinyl-N-methylformamide.

At the other chain end of the polyethers is a hydroxyl group, a hydroxyl group etherified with an organyl radical R or the hydroxyl group esterified with an acyl radical of the general structure R- (C =O) -, wherein the organyl radical R- is a C- - to C | | Q-

Alkyl group or a Cg- to C- | Q is alkylaryl group and may be linear or branched. Preference is given to hydroxyl, etherified hydroxyl group with methyl, ethyl-n-propyl, isopropyl, n-butyl, isobutyl, n-pentyl, 2-methylbutyl, 2,2-dimethylpropyl- , and n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl or the isomers of these radicals as alkyl radicals.

Particularly preferred are surfactants of the following formula:

Wherein the alkylene glycol units (C ₂ H ₄ O) and (C _q H _2q O) can be distributed randomly, in block form or as a gradient, and

R ¹ -H or -CH ₃

R2 is a -C = 0 group or an alkylene group from the group of methylene or ethylene, R3 is -H, linear or branched C- | - to Cg-alkyl or Cg- to Cg-alkylaryl,

p = 0 or 1,

q for a number from 3 to 4 and

n and m is a number from 1 to 20.

Particular preference is given to statistical or gradient structures such as, for example, hydroxy-functional surfactants such as Blemmer®50PEP-300 (polyalkylene glycol monomethacrylate, 3.5 ethylene glycol units and 2.5 propylene glycol units), Blemmer®55PET® 800 (polyalkylene glycol monomethacrylate, 10 ethylene glycol units and 5 butylene glycol units),

In a further preferred embodiment, block structures such. Blemmer® 70PEP-350B (polyalkylene glycol monomethacrylate; 5 ethylene glycol units and 2 terminal propylene glycol units) all used by NOF Corporation (Japan).

Further examples which may be mentioned of the block copolymers of polymerizable surfactants having an alkyl ether radical are as follows: methoxy-polyalkylene glycol mono (meth) acrylate (6 ethylene glycol units and 6 terminal propylene glycol units, both as ethylene glycol units and 3 terminal propylene glycol units) and butoxy Polyalkylene glycol mono (meth) acrylate (4 propylene glycol units and 7 terminal ethylene glycol units) from Evonik Industries AG.

In a further embodiment, the allylic surfactants may also be present in a random structure, e.g. (Polyalkylene glycol monoallyl ether, 7 ethylene glycol units and 3 propylene glycol units) (PE8482 Evonik Indusries AG).

As blowing agent, it is possible to use all carbonates from the group of lithium, sodium, potassium, rubidium, cesium carbonate or higher-valence metal ions such as beryllium, calcium, magnesium, strontium carbonate or mixtures thereof. As further compounds, it is also possible to use granulated carbonates which are also used as mixed salts of a carbonate and / or percarbonate with another salt which acts as a cover layer, such as, for example, B. a sulfate compound can be produced. According to the invention, the blowing agents have a particle size of from 10 .mu.m to 900 .mu.m, preferably from 50 .mu.m to 500 .mu.m, and more preferably from 100 .mu.m to 450 .mu.m. The carbonate compounds can be used as powder or in the form of their aqueous solution.

According to the invention, the surfactants are generally used simultaneously with the crosslinker. The blowing agent is added in one embodiment after the addition of the surfactant. In further embodiments, the blowing agent may be supplied at the same time or before the surfactant.

When blowing agents or soda are added, bubbles form, which have a smaller diameter in the presence of surfactants

According to the invention, the surfactants stabilize the large gas surface formed in the solution by the blowing agent. Due to the parallel polymerization, a fine-pored structure is fixed (porous gel). The surfactants are "inactivated" during the polymerization, ie they can be incorporated into the polymer network or incorporated due to their reactive functionality. The observed synergy between surfactants and blowing agents advantageously allows the use of minor amounts of blowing agent such as carbonate. Typical disadvantages associated with carbonates include the potential difficulties in mixing and addition in the solution, as well as uncontrolled dispersion of the resulting bubbles, such as high coalescence or bubbles, or loss of other properties of the SAP.

The monoethylenically unsaturated acid group-containing monomers (a1) may be partially or completely, preferably partially neutralized. The monoethylenically unsaturated monomers containing acid groups are preferably neutralized to at least 10 mol%, particularly preferably to 25 to 90 mol% and moreover preferably to 50-80 mol%. The neutralization of the monomers (a1) can take place before, but also after the polymerization. Here, the partial neutralization is carried out to at least 10 mol%, more preferably from 25 to 90 mol% and more preferably neutralized to 50-80 mol%. Furthermore, the neutralization can be carried out with alkali metal hydroxides, alkaline earth metal hydroxides, ammonia and carbonates and bicarbonates. In addition, every other base is conceivable, which forms a water-soluble salt with the acid. Also a mixed neutralization with different bases is conceivable. Preference is given to neutralization with ammonia or with alkali metal hydroxides, particularly preferably with sodium hydroxide or with ammonia.

Furthermore, in the case of a polymer, the free acid groups may predominate, so that this polymer has a pH lying in the acidic range. This acidic water-absorbing polymer may be at least partially neutralized by a polymer having free basic groups, preferably amine groups, which is basic as compared to the acidic polymer. These polymers are referred to in the literature as Mixed-Bed Ion-Exchange Absorbent Polymers (MBIEA polymers) and are disclosed inter alia in WO 99/34843 The disclosure of WO 99/34843 is hereby incorporated by reference and thus applies As a general rule, MBIEA polymers are a composition comprising, on the one hand, basic polymers capable of exchanging anions and, on the other hand, cations which are acidic in comparison to the basic polymer The basic polymer has basic groups and is typically obtained by the polymerization of monomers bearing basic groups or groups which can be converted to basic groups , secondary or tertiary amines or the corresponding phosphines or at least two of the above functional groups of monomers include, in particular, ethyleneamine, allylamine, diallylamine, 4-aminobutene, alkyloxycycline, vinylformamide, 5-aminopentene, carbodiimide, formaldacin, melamine and the like, and their secondary or tertiary amine derivatives. Preferred monoethylenically unsaturated acid group-containing monomers (a1) are acrylic acid, methacrylic acid, ethacrylic acid, α-chloroacrylic acid, α-cyanoacrylic acid, β-methylacrylic acid (crotonic acid), α-phenylacrylic acid, β-acryloxypropionic acid, sorbic acid, α-chlorosorbic acid, 2'-methylisocrotonic acid, Cinnamic acid, p-chlorocinnamic acid, β-stearylacrylic acid, itaconic acid, citraconic acid, mesaconic acid, glutaconic acid, aconitic acid, maleic acid, fumaric acid, tricarboxyethylene and maleic anhydride, with acrylic acid and methacrylic acid being particularly preferred, and acrylic acid being more preferred.

In addition to these carboxylate-containing monomers, preferred monoethylenically unsaturated acid group-containing monomers (a1) are ethylenically unsaturated sulfonic acid monomers or ethylenically unsaturated phosphonic acid monomers.

Preferred ethylenically unsaturated sulfonic acid monomers are allylsulfonic acid or aliphatic or aromatic vinylsulfonic acids or acrylic or methacrylic sulfonic acids. As aliphatic or aromatic vinylsulfonic acids, vinylsulfonic acid, 4-vinylbenzenesulfonic acid, vinyltoluenesulfonic acid and styrenesulfonic acid are preferred. As acrylic or methacrylic sulfonic acids, preference is given to sulfoethyl (meth) acrylate, sulfopropyl (meth) acrylate, 2-hydroxy-3-methacryloxypropylsulfonic acid and (meth) acrylamidoalkylsulfonic acids, such as 2-acrylamido-2-methylpropanesulfonic acid.

Preferred ethylenically unsaturated phosphonic acid monomers are vinylphosphonic acid, allylphosphonic acid, vinylbenzylphosphonic acid, (meth) acrylamidoalkylphosphonic acids, acrylamidoalkyldiphosphonic acids, phosponomethylated vinylamines and (meth) acrylicphosphonic acid derivatives.

As ethylenically unsaturated, a protonated nitrogen-containing monomers (a1) are preferably dialkylaminoalkyl (meth) acrylates in protonated form, for example dimethylaminoethyl (meth) acrylate hydrochloride or dimethylaminoethyl (meth) acrylate hydrosulfate, and dialkylaminoalkyl (meth) acrylamides in protonated form, for example, dimethylaminoethyl (meth) acrylamide hydrochloride, diemethylaminopropyl (meth) acrylamide hydrochloride, dimethylaminopropyl (meth) acrylamide hydrosulfate or dimethylaminoethyl (meth) acrylamide hydrosulfate.

Ethylenically unsaturated monomers (a1) containing a quaternized nitrogen are dialkylammoniumalkyl (meth) acrylates in quaternized form, for example trimethylammonium methyl (meth) acrylate methosulfate or dimethylethylammoniumethyl (meth) acrylate ethosulfate and also (meth) acrylamido-alkyldialkylamines quaternized form, for example (Meth) acrylamidopropyltrimethylammonium chloride, trimethylammoniumethyl (meth) acrylate chloride or (meth) aci lamidopropyltrimethylammoniumsulfat preferred.

As monoethylenically unsaturated monomers (a2) which can be copolymerized with (a1), preference is given to acrylamides and methacrylamides.

Preferred (meth) acrylamides are acrylamide and methacrylamide alkyl-substituted (meth) acrylamides or aminoalkyl-substituted derivatives of (meth) acrylamide, such as N-methylol (meth) acrylamide, N, N-dimethylamino (meth) acrylamide, dimethyl (meth) acrylamide or Diethyl (meth) acrylamide Possible vinylamides are, for example, N-vinylamides, N-vinylformamides, N-vinylacetamides, N-vinyl-N-methylacetamides, N-vinyl-N-methylformamides, vinylpyrrolidone. Particularly preferred among these monomers is acrylamide.

Further, as the monoethylenically unsaturated monomers (a2) copolymerizable with (a1), water-dispersible monomers are preferable. As the water-dispersible monomers, preferred are acrylic acid esters and methacrylic acid esters such as methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate or butyl (meth) acrylate, and vinyl acetate, styrene and isobutylene. Crosslinkers (a3) preferred according to the invention are compounds which have at least two ethylenically unsaturated groups within a molecule (crosslinker class I), compounds which have at least two functional groups which react with functional groups of the monomers (a1) or (a2) in a condensation reaction ( = Condensation crosslinker), in an addition reaction or in a ring-opening reaction (crosslinker class II), compounds containing at least one ethylenically unsaturated group and at least one functional group functionalized with groups of monomers (a1) or (a2) in a condensation reaction, in can react an addition reaction or in a ring-opening reaction (crosslinker III), or polyvalent metal cations (crosslinker class IV). Crosslinking of the polymers by the free radical polymerization of the ethylenically unsaturated groups of the crosslinker molecule with the monoethylenically unsaturated monomers (a1) or (a2) is achieved by the compounds of crosslinker class I, while in the compounds of crosslinker class II and the polyvalent metal cations of crosslinker class IV crosslinking of the polymers by condensation reaction of the functional groups (crosslinker class II) or by electrostatic interaction of the polyvalent metal cation (crosslinker class IV) with the functional groups of the monomers (a1) or (a2) is achieved. In the case of the compounds of the crosslinker class III, crosslinking of the polymer accordingly takes place both by free-radical polymerization of the ethylenic unsaturated group as well as by condensation reaction between the functional group of the crosslinker and the functional groups of the monomers (a1) or (a2).

Preferred compounds of crosslinker class I are poly (meth) acrylates which are obtained, for example, by the reaction of a polyol such as, for example, ethylene glycol, propylene glycol, trimethylolpropane, 1,6-hexanediol, glycerol, pentaerythritol, polyethylene glycol or polypropylene glycol, an aminoalcohol, a polyalkylenepolyamine, such as Diethylenetriamine or triethylenetetraamine, or an alkoxylated polyol can be recovered with acrylic acid or methacrylic acid. Further preferred compounds of crosslinker class I are polyvinyl compounds, poly (meth) allyl compounds, (meth) acrylic esters of a monovinyl compound or (meth) acrylic acid esters of a mono (meth) allyl compound, preferably of the mono (meth) allyl compounds of a polyol or of an aminoalcohol , In this context, reference is made to DE 195 43 366 and DE 195 43 368. The disclosures are hereby incorporated by reference and thus are considered part of the disclosure.

Examples of compounds of crosslinker class I are alkenyldi (meth) acrylates, for example ethylene glycol di (meth) acrylate, 1,3-propylene glycol di (meth) acrylate, 1,4-butylene glycol di (meth) acrylate, 1,3-butylene glycol di ( meth) acrylate, 1,6-hexanediol di (meth) acrylate, 1,1,10-decanediol di (meth) acrylate, 1,12-dodecanediol di (meth) acrylate, 1,18-octadecanediol di (meth) acrylate, cyclopentanediol di (meth) acrylate, neopentyl glycol di (meth) acrylate, methylenedi (meth) acrylate or pentaerythritol di (meth) acrylate, alkenyldi (meth) acrylamides, for example N-methyldi (meth) acrylamide, N, N'-3-methylbutylidenebis (meth) acrylamide, N, N '- (1, 2-dihydroxyethylene) bis (meth) acrylamide, N, N'-hexamethylene bis (meth) acrylamide or Ν, Ν'-methylenebis (meth) acrylamide, polyalkoxydi (meth) acrylates, for example diethylene glycol diol - (meth) acrylate, triethylene glycol di (meth) acrylate, tetraethylene glycol di (meth) acrylate, dipropylene glycol di (meth) acrylate, tripropylene glycol di (meth) acrylate or tetrapropylene glycol di (meth) acrylate, B isphenol A di (meth) acrylate, ethoxylated bisphenol A di (meth) acrylate, benzylidinedi (meth) acrylate, 1,3-di (meth) acryloyloxypropanol-2, hydroquinone di (meth) acrylate, di (meth) acrylate ester of preferably, with 1 to 30 moles of alkylene oxide per hydroxyl group oxyalkylated, preferably ethoxylated trimethylolpropane, Thioethylenglykoldi (meth) acrylate, thiopropylene glycol di (meth) acrylate, Thiopolyethylenglykoldi (meth) acrylate, thiopolypropylene glycol di (meth) acrylate, divinyl ether, for example 1 , 4-butanediol divinyl ether, divinyl esters, for example divinyl adipate, alkadienes, for example butadiene or 1,6-hexadiene, divinylbenzene, di (meth) allyl compounds, for example di (meth) allyl phthalate or di (meth) allyl succinate, homo- and copolymers of di (meth ) allyldimethylammonium chloride and homopolymers and copolymers of diethyl (meth) allylaminomethyl (meth) acrylate ammonium chloride, vinyl (meth) acryl compounds, for example vinyl (meth) acrylate, (meth) allyl (meth) acrylate Connections, for example se (meth) allyl (meth) acrylate, having 1 to 30 Mol of ethylene oxide per hydroxyl group ethoxylated (meth) allyl (meth) acrylate, di (meth) allyl esters of polycarboxylic acids, for example di (meth) allyl maleate, di (meth) allyfumarate, di (meth) allyl succinate or di (meth) allyl terephthalate, compounds with 3 or more ethylenically unsaturated, radically polymerizable groups such as glycerol tri (meth) acrylate, (meth) acrylate ester of preferably with 1 to 30 moles of ethylene oxide per hydroxylated oxyethylated glycerol, trimethylolpropane tri (meth) acrylate, tri (meth) acrylate ester of preferably 1 to 30 Moles of alkylene oxide per hydroxyl group oxyalkylated, preferably ethoxylated trimethylolpropane, trimethacrylamide, (meth) allylidenedi (meth) acrylate, 3-allyloxy-1,2-propanediol di (meth) acrylate, tri (meth) allyl cyanurate, tri (meth) allyl isocyanurate, Pentaerythritol tetra (meth) acrylate, pentaerythritol tri (meth) acrylate, (meth) acrylic acid ester of pentaerythritol oxyethylated with preferably 1 to 30 moles of ethylene oxide per hydroxyl group, tris (2 -hydroxyethyl) isocyanurate tri (meth) acrylate, trivinyl trimellitate, tri (meth) allylamine, di (meth) allylalkylamines, for example di (meth) allylmethylamine, tri (meth) allyl phosphate, tetra (meth) allylethylenediamine, poly (meth) allyl esters , Tetra (meth) allyloxi- ethane or tetra (meth) allylammoniumhalide.

Preferred compounds of crosslinker class II are compounds which have at least two functional groups which are preferred in a condensation reaction (= condensation initiator), in an addition reaction or in a ring-opening reaction with the functional groups of the monomers (a1) or (a2) with acid groups that can react monomers (a1). These functional groups of the compounds of crosslinker class II are preferably alcohol, amine, aldehyde, glycidyl, isocyanate, carbonate or epichloro functions.

Examples of compounds of crosslinker class II are polyols, for example ethylene glycol, polyethylene glycols such as diethylene glycol, triethylene glycol and tetraethylene glycol, propylene glycol, polypropylene glycols such as dipropylene glycol, tripropylene glycol or tetrapropylene glycol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, 2,4-pentanediol, 1,6-hexanediol, 2,5-hexanediol, glycerol, polyglycerol, trimethylolpropane, polyoxypropylene, oxyethylene-oxypropylene block copolymers, sorbitan fatty acid esters, polyoxyethylene sorbitan fatty acid esters, pentaerythritol, polyvinyl alcohol and sorbitol, amino alcohols, for example ethanolamine, diethanolamine , Triethanolamine or propanolamine, polyamine compounds, for example ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentaamine or pentaethylenehexaamine, polyglycidyl ether compounds such as ethylene glycol diglycidyl ether, polyethylene glycol diglycidyl ether, glycerol diglycidyl ether, glycerol polyglycidyl ether, pentareritritpoly glycidyl ethers, propylene glycol diglycidyl ethers, polypropylene glycol diglycidyl ethers, neopentyl glycol diglycidyl ethers, hexanediol glycidyl ethers, trimethylolpropane polyglycidyl ethers, sorbitol polyglycidyl ethers, diglycidyl diglycidyl esters, adipic acid diglycidyl esters, 1,4-phenylene bis (2-oxazoline), glycidol, polyisocyanates, preferably diisocyanates, such as 2,4- Toluene diisocyanate and hexamethylene diisocyanate, polyaziridine compounds such as 2,2-bishydroxymethylbutanol-tris [3- (1 -aziridinyl) propionate], 1, 6-hexamethylenediethyleneurea and ^{diphenylmethane-bis-4,4'-N,} N ^{'-diethylenharnstoff,} for example Halogenperoxide Epichloro- and epibromohydrin and α-methylepichlorohydrin, alkylene carbonates such as 1,3-dioxolan-2-one (ethylene carbonate), 4-methyl-1,3-dioxolan-2-one (propylene carbonate), 4,5-dimethyl-1,3 dioxolan-2-one, 4,4-dimethyl-1,3-dioxolan-2-one, 4-ethyl-1,3-dioxolan-2-one, 4-hydroxymethyl-1,3-dioxolan-2-one , 1, 3-dioxan-2-one, 4-methyl-1, 3-dioxan-2-one, 4,6-dimethyl-1,3-dioxan-2-one, poly-1,3-dioxolane-2 -on, polyquaternary amines such as condensation products of dimethylamines and epichlorohydrin. Further preferred compounds of crosslinker class II are polyoxazolines such as 1,2-ethylenebisoxazoline, crosslinkers with silane groups such as .gamma.-glycidoxypropyltrimethoxysilane and .gamma.-aminopropyltrimethoxysilane, oxazolidinones such as 2-oxazolidinone, bis- and poly-2-oxazolidinones and diglycol silicates.

As compounds of class III are hydroxyl- or amino-containing esters of (meth) acrylic acid, such as 2-hydroxyethyl (meth) acrylate and 2-hydroxypropyl (meth) acrylate and hydroxyl- or amino-containing (meth) acrylamides or mono (meth) allyl compounds of diols preferred.

The polyvalent metal cations of crosslinker class IV are preferably derived from mono- or polyvalent cations, the monovalent particular of alkali metals such as potassium, sodium, lithium, with lithium being preferred. Preferred divalent cations are derived from zinc, beryllium, alkaline earth metals such as magnesium, calcium, strontium, with magnesium being preferred. Further higher-grade cations which can be used according to the invention are cations of aluminum, iron, chromium, manganese, titanium, zirconium and other transition metals, as well as double salts of such cations or mixtures of the abovementioned salts. Preference is given to aluminum salts and alums and their different hydrates such. B. AICI3 x 6H ₂ 0, NaAl (S0 ₄ ) ₂ * 12 H ₂ 0, KAI (S0 ₄ ) ₂ * 12 H ₂ 0 or AI ₂ (S0 ₄ ) ₃ x14-18 H ₂ 0 used. Al ₂ (SO ₄ ) ₃ and its hydrates are particularly preferably used as crosslinker of crosslinking class IV.

The superabsorbent particles used in the process according to the invention are preferably crosslinked by crosslinkers of the following crosslinker classes or by crosslinkers of the following combinations of crosslinker classes: I, II, III, IV, III, II II, IV, IIIIII, III IV, II II IV, II I II IV, II IV or III IV. The above combinations of crosslinker classes each represent a preferred embodiment of crosslinkers of a superabsorbent particle used in the process according to the invention.

Further preferred embodiments of the superabsorbent particles used in the process according to the invention are polymers obtained by any of the abovementioned Crosslinkers of the crosslinker class I are networked. Among them, water-soluble crosslinkers are preferred. In this context, N, N ^{'methylenebisacrylamide,} polyethylene glycol di (meth) acrylates, triallylmethylammonium chloride, Tetraallylammoniumchlo- chloride and with 9 moles of ethylene oxide per mole of acrylic acid produced Allylnonaethylenglykolacrylat particularly preferred.

As water-soluble polymers (a4), water-soluble polymers such as partially or fully saponified polyvinyl alcohol, polyvinylpyrrolidone, starch or starch derivatives, polyglycols or polyacrylic acid may be present in the SAP particles, preferably in copolymerized form. The molecular weight of these polymers is not critical as long as they are water-soluble. Preferred water-soluble polymers are starch or starch derivatives or polyvinyl alcohol. The water-soluble polymers, preferably synthetic, such as polyvinyl alcohol, can also serve as a grafting base for the monomers to be polymerized. As auxiliaries (a5), in the polymers, organic or inorganic particles such as odor binders, in particular zeolites or cyclodextrins, skin care substances, surface-active agents or antioxidants are included.

The preferred organic excipients include cyclodextrins or their derivatives and polysaccharides. In addition, cellulose and cellulose derivatives such as CMC, cellulose ethers are preferred. Preferred cyclodextrins or cyclodextrin derivatives are those compounds which are disclosed in DE-A-198 25 486 on page 3, line 51 to page 4, line 61. The aforementioned section of this published patent application is hereby incorporated by reference and is considered part of the disclosure of the present invention. Particularly preferred cyclodextrins are non-derivatized α-, β-, γ- or δ-cyclodextrins.

As inorganic particulate adjuvants, it is possible to use all materials which are customarily used for modifying the properties of water-absorbing polymers. The preferred inorganic auxiliaries include sulfates such as Na ₂ SO ₄ , lactates such as sodium lactate, silicates, in particular skeletal silicates such as zeolites or silicates obtained by drying aqueous silica solutions or silica sols, for example the commercially available products such as precipitated silicas and fumed silicas, for example aerosils having a particle size in the range of 5 to 50 nm, preferably in the range of 8 to 20 nm, such as "Aerosil 200" from Evonik Industries AG, aluminates, titanium dioxides, zinc oxides, clay materials and other minerals familiar to the person skilled in the art, and also carbonaceous inorganic materials. Preferred silicates are all natural or synthetic silicates described in Hollemann and Wiberg, Lehrbuch der Anorganischen Chemie, Walter de Gruyter-Verlag, 91.-100. Edition, 1985 on pages 750 to 783, as silicates are disclosed. The foregoing section of this textbook is hereby incorporated by reference and is considered part of the disclosure of the present invention.

Particularly preferred silicates are the zeolites. As zeolites, it is possible to use all synthetic or natural zeolites known to the person skilled in the art. Preferred natural zeolites are zeolites of the natrolite group, the harmotome group, the mordenite group, the chabazite group, the faujasite group (sodalite group) or the analcite group. Examples of natural zeolites are Analcim, Leucite, Pollucite, Wairakite, Bellbergite, Bikitaite, Boggsite, Brewsterite, Chabazite, Willhendersonite, Cowlesite, Dachiardite, Edingtonite, Epistilbit, Erionite, Faujasite, Ferrierite, Amicite, Garronite, Gismondine, Gobbinsite, Gmelinite, Gonnardite , Goosecreekite, Harmotom, Phillipsite, Wellsite, Clinoptilolite, Heulandite, Laumontite, Levyne, Mazzite, Merlinoite, Montesommaite, Mordenite, Mesolite, Natrolite, Scolecite, Offretite, Paranatrolite, Paulingite, Perlialite, Barrerite, Stilbite, Stellerite, Thomsonite, Chernichite or Yugawaralite , Preferred synthetic zeolites are zeolite A, zeolite X, zeolite Y, zeolite P or the product ABSCENTS®. As zeolites, zeolites of the so-called "middle" type can be used, in which the Si0 ₂ / Al0 ₂ ratio is less than 10, particularly preferably the Si0 ₂ / Al0 ₂ - ratio of these zeolites in a range of 2 to 10. In addition to these "intermediate" zeolites, zeolites of the "high" type can be used further to which "include molecular sieve" zeolites of the ZSM, and zeolite beta. This "example, the known high" zeolites are preferably through a Si0 ₂ / Al0 ₂ Ratio of at least 35, more preferably characterized by a Si0 ₂ / Al0 ₂ ratio in a range of 200 to 500.

The aluminates used are preferably naturally occurring spinels, in particular ordinary spinel, zinc spinel, iron spinel or chromium spinel.

Preferred titanium dioxide is the pure titanium dioxide in the rutile, anatase and brookite crystal forms, as well as iron-containing titanium dioxides such as ilmenite, calcium-containing titanium dioxides such as titanite or perovskite.

Preferred clay materials are those described in Hollemann and Wiberg, Lehrbuch der Inorganischen Chemie, Walter de Gruyter-Verlag, 91.-100. Edition, 1985 pages 783 to 785, are disclosed as clay materials. The above section of this textbook is hereby incorporated by reference and is considered part of the Disclosure of the present invention. Particularly preferred clay materials are kaolinite, lllite, halloysite, montmorillonite and talc.

Furthermore, as inorganic fine particles, the metal salts of mono-, oligo- and polyphosphoric acids are preferred according to the invention. Of these, in particular the hydrates are preferred, with the mono- to deca-hydrates and tri-hydrates being particularly preferred. Suitable metals are, in particular, alkali metals and alkaline earth metals, the alkaline earth metals being preferred. Among them, Mg and Ca are preferable, and Mg is particularly preferable. In connection with phosphates, phosphoric acids and their metal compounds is on Hollemann and Wiberg, Textbook of Inorganic Chemistry, Walter de Gruyter-Verlag, 91.-100. Edition, 1985, on pages 651-669. The foregoing section of this textbook is hereby incorporated by reference and is considered part of the disclosure of the present invention. Preferred carbonaceous but not organic auxiliaries are those pure carbons which are described in Hollemann and Wiberg, Lehrbuch der Anorganischen Chemie, Walter de Gruyter-Verlag, 91.-100. Edition, 1985 on pages 705 to 708 are called Graphite. The foregoing section of this textbook is hereby incorporated by reference and is considered part of the disclosure of the present invention. Particularly preferred graphites are artificial graphites such as coke, pyrographite, activated carbon or carbon black.

The water-absorbing polymers obtained in the process according to the invention are preferably obtainable by first producing a hydrogel polymer (VP) in particulate form from the abovementioned monomers and crosslinkers. The preparation of this starting material for the water-absorbing polymers is carried out, for example, by bulk polymerization, which preferably takes place in kneading reactors such as extruders, solution polymerization, spray polymerization, inverse emulsion polymerization or inverse suspension polymerization. The solution polymerization is preferably carried out in water as solvent. The solution polymerization can be continuous or discontinuous. From the prior art, a wide range of possible variations in terms of reaction conditions such as temperatures, type and amount of initiators and the reaction solution can be found. Typical processes are described in the following patents: US 4,286,082, DE 27 06 135, US 4,076,663, DE 35 03 458, DE 40 20 780, DE 42 44 548, DE 43 23 001, DE 43 33 056, DE 44 18 818. The disclosures are hereby incorporated by reference and thus are considered part of the disclosure. As initiators for the initiation of the polymerization, it is possible to use all initiators which form free radicals under the polymerization conditions and which are customarily used in the production of superabsorbers. These include thermal initiators, redox initiators and photoinitiators whose activation is effected by high-energy radiation. The polymerization initiators may be dissolved or dispersed in a solution of monomers according to the invention. The use of water-soluble initiators is preferred.

Suitable thermal initiators are all compounds known to the person skilled in the art and decomposing into free radicals under the influence of temperature. Particular preference is given here to thermal polymerization initiators having a half-life of less than 10 seconds, moreover preferably less than 5 seconds at less than 180 ° C., more preferably less than 140 ° C. Peroxides, hydroperoxides, hydrogen peroxide, persulfates and azo compounds are particularly preferred thermal polymerization initiators. In some cases it is advantageous to use mixtures of different thermal polymerization initiators. Among these mixtures, those of hydrogen peroxide and sodium or potassium peroxodisulfate are preferred, which can be used in any conceivable quantitative ratio. Suitable organic peroxides are preferably acetylacetone peroxide, methyl ethyl ketone peroxide, benzoyl peroxide, lauroyl peroxide, acetyl peroxide, capric peroxide, isopropyl peroxydicarbonate, 2-ethylhexyl peroxydicarbonate, t-butyl hydroperoxide, cumene hydroperoxide, t-amyl perpivalate, t-butyl perpivalate, t-butyl perohexonate, t-butyl isobutyrate, t-butyl per-2 ethylhexenoate, t-butyl perisononanoate, t-butyl permaleate, t-butyl perbenzoate, t-butyl-3,5,5-tri-methylhexanoate and amylperneodecanoate. Additionally preferred as the thermal polymerization initiators are: azo compounds such as Azobisisobutyronitrol, azobisdimethylvaleronitrile, 2,2 - azobis (2-amidinopropane) dihydrochloride, azo-bis-amidinopropane dihydrochloride, ^2,2'-azobis N-dimethylene (N, ) isobutyramidine dihydrochloride, 2- (carbamoylazo) - isobutyronitrile and 4,4 ^'- azobis (4-cyanovaleric acid). The compounds mentioned are used in conventional amounts, preferably in a range from 0.01 to 5, preferably from 0.1 to 2 mol%, in each case based on the amount of the monomers to be polymerized.

The redox initiators contain as oxidic component at least one of the abovementioned per compounds and as reducing component preferably ascorbic acid, glucose, sorbose, manose, ammonium or alkali metal hydrogensulfite, - sulfate, thiosulfate, hyposulfite or sulfide, metal salts such as iron-II ions or silver ions or sodium hydroxymethylsulfoxylate. As reducing component of the redox initiator, ascorbic acid or sodium pyrosulfite is preferably used. Based on the amount of monomers used in the polymerization is 1 x 10 ^"5 to 1 mol% of the reducing component of the redox initiator and 1 x 10 ^{" 5} to 5 mol% of the oxidizing Component of the redox initiator used. Instead of or in addition to the oxidizing component of the redox initiator, one or more, preferably water-soluble, azo compounds can be used. When the polymerization is triggered by the action of high-energy radiation, so-called photoinitiators are usually used as the initiator. These may be, for example, so-called a-splitters, H-abstracting systems or even azides. Examples of such initiators are benzophenone derivatives such as Michler's ketone, phenanthrene derivatives, fluorene derivatives, anthraquinone derivatives, thioxanthone derivatives, coumarin derivatives, benzoin ethers and their derivatives, azo compounds such as the abovementioned radical formers, substituted hexaarylbisimidazoles or acylphosphine oxides. Examples of azides are: 2- (N, N-dimethylamino) ethyl-4-azidocinnamate, 2- (N, N-dimethylamino) ethyl-4-azidonaphthyl ketone, 2- (N, N-dimethylamino) ethyl-4 -azidobenzoate, 5-azido-1-naphthyl-2 '- (N, N-dimethylamino) ethylsulfone, N- (4-sulfonylazidophenyl) maleimide, N-acetyl-4-sulfonylazidoaniline, 4-sulfonylazidoaniline, 4-azidoaniline, 4-azidophenacyl bromide, p-azidobenzoic acid, 2,6-bis (p-azidobenzylidene) cyclohexanone and 2,6-bis (p-azidobenzylidene) -4-methylcyclohexanone. The photoinitiators, if used, are usually used in amounts of 0.01 to 5 wt .-%, based on the monomers to be polymerized.

According to the invention, preference is given to using an initiator system consisting of hydrogen peroxide, sodium peroxodisulfate and ascorbic acid. In general, the polymerization is initiated with the initiators in a temperature range from 0 ° C to 90 ° C. The polymerization reaction may be initiated by one initiator or by several co-acting initiators. Furthermore, the polymerization can be carried out in such a way that one first adds one or more redox initiators. In the further course of polymerization, thermal initiators or photoinitiators are then additionally applied, wherein in the case of photoinitiators the polymerization reaction is then initiated by the action of high-energy radiation. The reverse order, ie the initial initiation of the reaction by means of high-energy radiation and photoinitiators or thermal initiators, and initiation of the polymerization by means of one or more redox initiators taking place in the further course of polymerization is also conceivable.

In order to convert the hydrogel polymers (VP) thus obtained into a particulate form, these can, after their separation from the reaction mixture, first at a temperature in a range of 20 to 300 ° C, preferably in a range of 50 to 250 ° C and more preferably in a range of 100 to 200 ° C to a water content of less than 40 wt .-%, preferably less than 20 wt .-% and furthermore preferably less than 10% by weight, in each case based on the total weight of the hydrogel polymer (VP), are dried. Drying is preferably carried out in ovens or dryers known to those skilled in the art, for example in belt dryers, tray dryers, rotary kilns, fluid bed dryers, plate dryers, paddle dryers or infrared dryers.

According to the present invention, the comminution is preferably carried out by dry milling, preferably by dry milling in a hammer mill, a pin mill, a ball mill or a roller mill. In a further embodiment of the present invention, the comminution of the hydrogel polymer can also be effected by the combinations of several of the above-described mills.

In a preferred embodiment of the process according to the invention, particles which have an inner region and a surface region bounding the inner region are obtained as water-absorbing polymers. The surface area has a different chemical composition than the interior area or differs in a physical property from the inside area. Physical properties in which the interior differs from the surface area are, for example, the charge density or the degree of crosslinking.

These water-absorbing polymers having an inner region and an inner region-limiting surface area are preferably obtainable by postcrosslinking near-surface, reactive groups of the particles of the hydrogel polymer (VP). This postcrosslinking can be effected thermally, photochemically or chemically.

As postcrosslinkers, preference is given to the compounds of crosslinker class II and IV mentioned in connection with crosslinkers (a3). Preferred secondary crosslinkers are diethylene glycol, triethylene glycol, polyethylene glycol, glycerol, polyglycerol, propylene glycol, diethanolamine, triethanolamine, polyoxypropylene, oxyethylene-oxypropylene Block copolymers, sorbitan fatty acid esters, polyoxyethylene sorbitan fatty acid esters, trimethylolpropane, pentaerythritol, polyvinyl alcohol, sorbitol, 1,3-dioxolan-2-one (ethylene carbonate), 4-methyl-1,3-dioxolan-2-one (propylene carbonate), 4,5 -Dimethyl-1,3-dioxolan-2-one, 4,4-dimethyl-1,3-dioxolan-2-one, 4-ethyl-1,3-dioxolan-2-one, 4-hydroxymethyl-1,3 -dioxolan-2-one, 1, 3-dioxan-2-one, 4-methyl-1,3-dioxan-2-one, 4,6-dimethyl-1,3-dioxan-2-one, 1,3 Dioxolan-2-one, poly-1,3-dioxolan-2-one. Ethylene carbonate is particularly preferably used as postcrosslinker. Preferred embodiments of the water-absorbing polymers are those which are postcrosslinked by crosslinkers of the following crosslinker classes or by crosslinkers of the following combinations of crosslinker classes: II, IV and II IV.

Preferably, the postcrosslinker is used in an amount ranging from 0.01 to 30% by weight, more preferably in an amount ranging from 0.1 to 20% by weight, and more preferably in an amount within a range of 0.3 to 5 wt .-%, each based on the weight of the superabsorbent polymers used in the post-crosslinking.

It is likewise preferred that the postcrosslinking is effected by using a solvent, comprising preferably water, water-miscible organic solvents such as methanol or ethanol or mixtures of at least two thereof, and the postcrosslinker with the outside area of the hydrogel polymer particles at a temperature in a range of 30 to 300 ^° C, more preferably in a range of 100 to 200 ^° C are brought into contact. The bringing into contact is preferably effected by spraying, the mixture consisting of postcrosslinker and solvent, on the hydrogel polymer particles and subsequent mixing of the hydrogel polymer particles brought into contact with the mixture. In this case, the postcrosslinker in the mixture is preferably in an amount in a range of 0.01 to 20 wt .-%, particularly preferably in an amount in a range of 0.1 to 10 wt .-%, based on the total weight of the mixture , contain. It is further preferred that in an amount in a range of 0.01 to 50 wt .-%, particularly preferably in an amount in a range of 0.1 to 30 wt .-%, each based on the weight of the hydrogel Polymer particles, is brought into contact with the hydrogel polymer particles.

Suitable condensation reactions are preferably the formation of ester, amide, imide or urethane bonds, the formation of ester bond being preferred.

In addition, other additives and effect substances can be added to the hydrogel polymers according to the invention and / or water-absorbing polymers.

Further preferred release agents are release agents, such as inorganic or organic powder release agents. These release agents are preferably used in amounts ranging from 0 to 2% by weight, more preferably in a range of 0.1 to 1.5% by weight, based on the weight of the hydrogel polymer and / or the water-absorbent polymer used. Preferred release agents are wood flour, pulp fibers, powdered bark, cellulose powder, mineral fillers such as perlite, synthetic fillers such as nylon powder, rayon powder, diatomaceous earth, bentonite, kaolin, zeolites, talc, loam, Ash, coal dust, magnesium silicates, fertilizers or mixtures of substances. Highly dispersed pyrogenic silica, as sold under the trade name Aerosil by Evonik Degussa, is preferred. In a further preferred embodiment of the method according to the invention, bringing the hydrogel polymer particles and / or the water-absorbing polymer particles into contact with an effect substance, such as a polysugar, a polyphenolic compound such as hydrolyzable tannins or a silicon-oxygen containing compound or a mixture of at least two effect materials based on it. The effect material can be added both in solid form (powder) and in dissolved form with a solvent, wherein the addition of the effect substance takes place at the earliest after process step iii). As effect material is understood in the context of the present invention, a substance which serves for odor inhibition. According to the invention, these are understood as meaning polyuclides in which the person skilled in the art understands those from the group of the known starches and their derivatives, celluloses and their derivatives, cyclodextrins, cyclodextrins being preferably understood as meaning cyclodextrin, .beta.-cyclodextrin, .gamma.-cyclodextrin or mixtures of these cyclodextrins ,

As the silicon-oxygen-containing compounds, zeolites are preferable. As zeolites, it is possible to use all synthetic or natural zeolites known to the person skilled in the art. Preferred natural zeolites are zeolites from the natolite group harmotome group, the mordenite group, the chabazite group, the faujasite group (sodalite group) or the analcite group. Examples of natural zeolites are Analcim, Leucite, Pollucite, Wairakite, Bellbergite, Bikitaite, Boggsite, Brewsterite, Chabazite, Willhersonite, Cowlesite, Dachiardite, Edingtonite, Epistilbit, Erionite, Faujasite, Ferrierite, Amicite, Garronite, Gismondine, Gobbinsite, Gmelinite, Gonnardite , Goosecreekite, Harmotom, Phillipsite, Wellsite, Clinoptilolite, Heulandite, Laumontite, Levyne, Mazzite, Merlinoite, Montesommaite, Mordenite, Mesolite, Natrolite, Scolecite, Offretite, Paranatrolite, Paulingite, Perlialite, Barrerite, Stilbite, Stellerite, Thomsonite, Chernichite or Yugawaralite , Preferred synthetic zeolites are zeolite A, zeolite X, zeolite Y, zeolite P or the product ABSCENTS®.

As cations, the zeolites used in the process according to the invention preferably contain alkali metal cations such as Li ⁺ , Na ⁺ , K ⁺ , Rb ⁺ , Cs ⁺ or Fr ⁺ and / or alkaline earth metal cations such as Mg ²⁺ , Ca ²⁺ , Sr ² * or Ba ²⁺ .

As zeolites zeolites of the so-called "middle" type can be used, in which the Si0 ₂ / Al0 ₂ ratio is less than 10, particularly preferably the Si0 ₂ / Al0 ₂ - In addition to these "middle" zeolites, zeolites of the "high" type can be used, which include, for example, the well-known "molecular sieve" zeolites of the type ZSM and zeolite beta. These "high" zeolites are preferably characterized by a Si0 ₂ / Al0 ₂ ratio of at least 35, more preferably of a Si0 ₂ / Al0 ₂ ratio in a range of 200 to 500.

Preferably, the zeolites are used as particles having an average particle size in a range from 1 to 500 μm, more preferably in a range from 2 to 200 μm, and moreover preferably in a range from 5 to 100 μm.

The effect substances are preferably used in the process according to the invention in an amount in a range from 0.1 to 50% by weight, more preferably in a range from 1 to 40% by weight and moreover preferably in an amount in the region of 5 to 30% by weight, based in each case on the weight of the hydrogel polymer particles and / or water-absorbing polymer particles.

As germ-inhibiting agents are in principle all active against Gram-positive bacteria substances such. 4-hydroxybenzoic acid and its salts and esters, N- (4-chlorophenyl) -N '- (3,4-dichlorophenyl) urea, 2,4,4'-trichloro-2'-hydroxydiphenyl ether (triclosan), 4- Chloro-3,5-dimethylphenol, 2,2'-methylenebis (6-bromo-4-chlorophenol), 3-methyl-4- (1-methylethyl) phenol, 2-benzyl-4-chlorophenol, 3- ( 4-chlorophenoxy) -1,2-propanediol, 3-iodo-2-propynyl butylcarbamate, chlorhexidine, 3,4,4'-trichlorocarbanilide (TTC), antibacterial fragrances, thymol, thyme oil, eugenol, clove oil, menthol, mint oil, farnesol, Phenoxyethanol, glycerol monocaprinate, glycerol monocaprylate, glycerol monolaurate (GML), diglycerol monocaprinate (DMC), salicylic acid N-alkylamides such as. Salicylic acid n-octylamide or salicylic acid n-decylamide.

For example, esterase inhibitors are suitable as enzyme inhibitors. These are preferably trialkyl citrates such as trimethyl citrate, tripropyl citrate, triisopropyl citrate, tributyl citrate and in particular triethyl citrate (Hydagen ™ CAT, Cognis GmbH, Dusseldorf / Germany). The substances inhibit the enzyme activity and thereby reduce odors. Further substances which are suitable as esterase inhibitors are sterol sulfates or phosphates, such as, for example, lanosterol, cholesterol, campesterol, stigmasterol and sitosterol sulfate or phosphate, dicarboxylic acids and their esters, for example glutaric acid, glutaric acid monoethyl ester, glutaric acid diethyl ester, adipic acid, Adipic acid monoethyl ester, diethyl adipate, malonic acid and diethyl malonate, hydroxycarboxylic acids and their esters such as citric acid, malic acid, tartaric acid or diethyl tartrate, and zinc glycinate. Suitable odor absorbers are substances that absorb and largely retain odor-forming compounds. They reduce the partial pressure of the individual components and thus also reduce their propagation speed. It is important that perfume must remain unimpaired. Odor absorbers have no activity against bacteria. They contain, for example, as a main component of a complex zinc salt of ricinoleic acid or special, largely odorless fragrances, which are known in the art as "fixatives", such. B. Extracts of Labdanum or Styrax or certain Abietinsäurederivate. Odor maskers are fragrances or perfume oils which, in addition to their function as odor maskers, give the deodorants their respective scent. Examples of perfume oils are mixtures of natural and synthetic fragrances. Natural fragrances are extracts of flowers, stems and leaves, fruits, fruit peel, roots, woods, herbs and grasses, needles and twigs, as well as resins and balsams. Furthermore, animal raw materials come into question, such as civet and Castoreum. Typical synthetic fragrance compounds are ester type products, ethers, aldehydes, ketones, alcohols and hydrocarbons. Fragrance compounds of the ester type are e.g. Benzyl acetate, p-tert-butylcyclohexyl acetate, linalyl acetate, phenylethyl acetate, linalyl benzoate, benzyl formate, allyl cyclohexyl propionate, styrallyl propionate and benzyl salicylate. The ethers include, for example, benzyl ethyl ether to the aldehydes z. B. the linear alkanals having 8 to 18 carbon atoms, citral, citronellal, citronellyloxyacetaldehyde, cyclamen aldehyde, hydroxycitronellal, lilial and bourgeonal, to the ketones z. The alcohols include anethole, citronellol, eugenol, isoeugenol, geraniol, linalool, phenylethyl alcohol and terpineol, the hydrocarbons include mainly the terpenes and balsams. Preferably, however, mixtures of different fragrances are used, which together produce an attractive fragrance. Also essential oils of lower volatility, which are mostly used as aroma components, are suitable as perfume oils, eg. B. sage oil, camomile oil, clove oil, lemon balm oil, mint oil, cinnamon oil, lime blossom oil, juniper berry oil, vetiver oil, oliban oil, galbanum oil, labdanum oil and lavandin oil. Preferably bergamot oil, dihydromyrcenol, lilial, lyral, citronellol, phenylethyl alcohol, alpha -Hexylzimtaldehyd, geraniol, benzylacetone, cyclamen aldehyde, linalool, Boisambrene Forte, Ambroxan, indole, hedione, Sandelice, citron oil, tangerine oil, orange oil, Allylamylglycolat, Cyclovertal, lavandin oil, Muscat Sage oil, beta-damascone, geranium oil bourbon, cyclohexyl salicylate, vertofix coeur, iso-e-super, fixolide NP, evernyl, iraldeine gamma, phenylacetic acid, geranyl acetate, benzyl acetate, rose oxide, romilate, irotyl and floramate alone or in mixtures.

Antiperspirants reduce sweating by affecting the activity of the eccrine sweat glands, thus counteracting underarm wetness and body odor. When Astringent antiperspirant active ingredients are especially suitable salts of aluminum, zirconium or zinc. Such suitable antiperspirant active ingredients are, for. For example, aluminum chloride, aluminum chlorohydrate, aluminum dichlorohydrate, Aluminiumiumsesqui- chlorohydrate and their complex compounds z. With propylene glycol-1, 2. Aluminiumhydroxyallantoinat, aluminum chloride tartrate, aluminum zirconium trichlorohydrate, aluminum zirconium tetrachlorohydrate, aluminum zirconium pentachlorohydrate and their complex compounds z. With amino acids such as glycine.

For mixing or spraying, all devices are suitable which allow a homogeneous distribution of a solution, powder, suspension or dispersion on or with the hydrogel polymer particles (VP) or water-absorbing polymers. Examples are Lödige mixers (manufactured by Gebrüder Lödige Maschinenbau GmbH), Gericke multi-flux mixers (manufactured by Gericke GmbH), DRAIS mixers (manufactured by DRAIS GmbH Spezialmaschinenfabrik Mannheim), Hosokawa mixers (Hosokawa Mokron Co. Ltd.), Ruberg mixers (manufactured by Gebr. Ruberg GmbH & Co. KG Nieheim), Hüttlin coaters (manufactured by BWI Hüttlin GmbH Steinen), fluidized bed dryers or spray granulators of AMMAG (manufactured by AMMAG Gunskirchen, Austria ) or Heinen (manufactured by A. Heinen AG Anlagenbau Varel), Patterson-Kelly mixers, NARA paddle mixers, screw mixers, plate mixers, fluidized bed dryers or Schugi mixers. For bringing into contact in a fluidized bed all known to those skilled and suitable appear fluidized bed method can be applied. For example, a fluidized bed coater can be used. A further contribution to the solution of the objects described at the outset is provided by a composite comprising the water-absorbing polymers according to the invention or the hydrogel polymers or the water-absorbing polymers or hydrogel polymers obtainable by the processes according to the invention and a substrate. It is preferred that the water-absorbing polymers or hydrogel polymers according to the invention and the substrate are firmly bonded together. As substrates, films of polymers, such as polyethylene, polypropylene or polyamide, metals, nonwovens, fluff, tissues, fabrics, natural or synthetic fibers, or foams are preferred. Furthermore, it is preferred according to the invention that the composite comprises at least one region of water-absorbing polymers or hydrogel polymers in an amount in the range of about 15 to 100 wt .-%, preferably about 30 to 100 wt .-%, particularly preferably of about 50 to 99.99 wt .-%, further preferably from about 60 to 99.99 wt .-% and more preferably from about 70 to 99 wt .-%, each based on the total weight of the relevant area of the composite includes, being this Range preferably has a size of at least 0.01 cm ³ , preferably at least 0.1 cm ³ and most preferably at least 0.5 cm ³ .

A further contribution to the solution of at least one of the abovementioned objects is provided by a process for producing a composite, wherein the water-absorbing polymers according to the invention or the superabsorbent obtainable by the process according to the invention and a substrate and optionally an additive are brought into contact with one another. The substrates used are preferably those substrates which have already been mentioned above in connection with the composite according to the invention.

A contribution to the solution of at least one of the abovementioned objects is also provided by a composite obtainable by the process described above, this composite preferably having the same properties as the composite according to the invention described above.

A further contribution to the solution of at least one of the abovementioned objects is provided by chemical products comprising the water-absorbing polymers or hydrogel polymers according to the invention or a composite according to the invention. Preferred chemical products are, in particular, foams, shaped articles, fibers, films, cables, sealing materials, liquid-absorbent hygiene articles, in particular diapers and sanitary napkins, carriers for plant- or fungi-growth-regulating agents or crop protection active ingredients, additives for building materials, packaging materials or floor additives. The use of the water-absorbing polymers or of the composite according to the invention in chemical products, preferably in the abovementioned chemical products, in particular in hygiene articles such as diapers or sanitary napkins, and the use of the water-absorbing polymer particles as a carrier for plant or fungi growth-regulating agents or crop protection active ingredients contribute to solve at least one of the objects mentioned above. When used as a carrier for plant or fungi growth regulating agents or crop protection actives, it is preferred that the plant or fungi growth regulating agents or crop protection actives can be delivered for a period of time controlled by the carrier. TEST METHODS

Unless otherwise stated below, the measurements herein are made according to the ERT method. "ERT" stands for EDANA Recommended Test and "EDANA" for European Disposable and Nonwoven Association All test methods are generally carried out at an ambient temperature of 23 + 2 ° C and a relative humidity of 50 + 10%, unless otherwise stated ,

Particle Size Distribution (PSD Particle Size Distribution)

The particle size distribution of the water-absorbing polymer particles is determined analogously to the EDANA-recommended test method no. WSP 220.3-10 "Particle Size Distribution".

Centrifuge Retention Capacity (CRC Centrifuge Retention Capacity)

Centrifuge retention capacity was determined according to the EDANA (European Disposables and Nonwovens Association) recommended test method no. WSP 241.3-10 "Centrifuge retention capacity".

Determination of the Free Swell Rate (FSR)

The absorption rate was determined by measuring the so-called "Free Swell Rate - FSR" according to the test method described in EP-A-0 443 627 on page 12.

Absorption against a pressure of 0.7 psi (AAP)

The absorption under pressure was determined as AAP (Absorption Against Pressure) according to WSP 242.3-10 on the total grain fraction. Accordingly, 0.90 g of the test substance (sieved between 150 and δδθμηη) in a test cylinder with 60.0 mm inner diameter and a sieve bottom (400 mesh) weighed (concentration: 0.032 g / cm ² ) and evenly distributed. A cylindrical weight of 50 g / cm ² = 0.7 psi) with an outside diameter of 59.2 mm is placed on the test substance. In a plastic bowl filter plates are placed, which are covered with a filter paper. The plastic dish is filled with 0.9% NaCl solution until the liquid level is flush with the top edge of the filter plates. Subsequently, the prepared measuring units are placed on the filter plates. After a swelling time of 60 minutes, the measuring units are removed and the weight removed. The amount of liquid absorbed is determined gravimetrically and converted to 1 gram of test substance. Determination of permeability (saline flow conductivitv - SFC)

The permeability is determined by measuring the so-called "Saline Flow Conductivity SFC" according to the test method described in WO-A-95 / 26209. The weight of the superabsorbent material is 1.5 g instead of 0.9 g.

Determination of "Fixed Height Absorption" (FHA) (0.3 psi, 20 cm)

The determination is made by measuring the so-called "fixed height absorption" (FHA) according to the test method described in EP 149 34 53 A1 on page 9 [0078] to page 10 paragraph [0087].

Determination of the surface tension (OFS)

The determination is made by the measurement according to the test method described in EP 1 493 453 A1 according to page 12 paragraph [0105] to [01 11]. A Kruss K1 1 tensiometer with a Wilhelmy plate was used.

Determination of the extractable polvether shares

The determination of the extractable fractions of the polyethers is based on the HPTLC method (H-lll 14a, as of 30.05.95) Joint work of the DGF 152 Communication. The samples were ground, extracted with methanol in Soxhlet warm (1 hour), concentrated and then determined by thin layer chromatography on TLC plates of silica gel 60 with the dimensions 20x 20 cm. The application of the samples is standardized. As a flow agent, a mixture of chloroform / methanol / water (88/1 1/1 volume percent) was used. The derivatization was carried out with the Dragendorffs reagent. A TLC scanner Camag CD60 with a measuring wavelength of 520 nm was used. The evaluation was carried out via the peak areas which were set in relation to the peak areas of the standards.

Determination of the "BET surface area"

The BET surface area of the superabsorbents was determined by means of a "tristar 3020 Kr" device from Micromeritics (with krypton gas instead of nitrogen) and worked analogously to ISO 9277. The initial weight was 4.6 g and was evacuated overnight at room temperature and a vacuum of 0.02 mbar and weighed back. Evacuation was performed at the analysis port with evacuation over a period of 6 minutes when 10mm HG was reached. The dead volume determination was also carried out. The analysis temperature was 77.1K. The pO was defined to be 2.32mmHG (using krypton gas). Equalization time for equilibrium was measured at least 10 times (5 sec, with a rate of change of less than 0.01%). Examples

The following examples serve to illustrate the invention without, however, limiting it thereto.

Table 1

Surfactant - Name Description Copolymer driven Beispiet (supplier) (including sequence of blocks, as far as

No. Applicable)

PE 8482

1 allyl ether - [(EO) 7- (PO) 3] -H Statistical

(Evonik Industries)

Blemmer®50PEP-300

2 Methacrylate esters - [(EO) 3,5- (PO) 2,5] -H Statistical

(NOF Corporation)

Blemmer @ 55PET-800

3 Methacrylate ester - [(EO) 10- (BO) 5] -H Statistical

(NOF Corporation)

Blemmer @ 70PEP-350B

4 Methacrylate ester- [EO] 5- [PO] 2-H as a block

(NOF Corporation)

Sodium lauryl ether sulfate

5 sodium lauryl ether sulfate - (Hansa-Group)

In the context of the present invention, the term "EO" basically refers to ethylene glycol unit. The term "PO" is understood to mean, in principle, propylene glycol unit and the term "BO" is basically understood to mean a butylene glycol unit.

The following examples according to the invention show the synergistic effect on the FSR value by the simultaneous use of polymerisable surfactants and carbonate. In this case, a defined particle size distribution (PSD) was used (150μηι to 710μη "ΐ) .As a standard mixture, a composition of 4 particle fractions is used before the surface postcrosslinking, which are distributed as follows: 15 wt.% Of a particle size of 150 m to 300μη-ι; 50% by weight 300μηι to δθθηη; 30% by weight 500μηι to 600μηι and 5% by weight 600μηι to 710μη "ΐ. The PSD is adjusted for the hydrogel polymers.

In EP 1 701786 B1, the particle diameter of the particle diameter is defined as D50 in paragraphs [01 15 to 01 17] According to the invention, a range between 300 and 600 μm is preferred, a range of 350 to 550 μm is particularly preferred, and very particularly preferred a range between 400 and δθθμηη. Preferred is a blowing agent, in which more than 35% by weight of the particles have a particle size of 100-300μηι.

The term "SX" as used in the description refers to the thermal surface postcrosslinking of the precursor (VP) the hydrogel polymer produced after the first drying, with the aforementioned particle size distribution.

In principle, the percentages of the surfactant are based on the acrylic acid (320 g unless mentioned otherwise) and that of the carbonate on the batch (normally 1000 g).

example 1

The surfactant No. 1 PE 8482 "allyl ether - [(EO) 7- (PO) 3] -H" from Table 1 was used as an additive The amounts of surfactant used varied Acrylic acid and that of the carbonate on the approach.

Use without polymerizable surfactant and soda:

Example A (reference)

In 975.762 g of an aqueous solution of sodium acrylate having a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 39.8%, 0.590 g of polyethylene glycol 300 diacrylate (0.15% based on acrylic acid / ester content corresponding to 81%) and 1 , 263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agents. The monomer solution was purged with nitrogen in a plastic polymerization vessel for 30 minutes to remove the dissolved oxygen. At a temperature of 4 ° C, the polymerization by the subsequent addition of 0.3 g of sodium peroxodisulfate in 10 g of dist. Water, 0.07 g of 35% hydrogen peroxide solution in 10 g of dist. Water and 0.015 g of ascorbic acid in 2 g of dist. Water started. After the final temperature (about 100 ° C) was reached, the gel was minced with a meat grinder and dried for 2 h at 150 ° C in a convection oven. The dried precursor was coarsely crushed, ground and adjusted to the above particle size distribution. Use without polymerizable surfactant and 0.1% soda slightly

Example B (reference)

In 974.762 g of an aqueous solution of sodium acrylate having a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 39.8%, 0.590 g of polyethylene glycol 300 diacrylate (0.15% based on acrylic acid / ester content corresponding to 81%) and 1 , 263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agents. The monomer solution was purged with nitrogen in a plastic polymerization vessel for 30 minutes to remove the dissolved To remove oxygen. At a temperature of 4 ° C, 1 g of finely calcined soda (Solvay) were added and the polymerization by the subsequent addition of 0.3 g of sodium peroxodisulfate in 10 g of dist. Water, 0.07 g of 35% hydrogen peroxide solution in 10 g of dist. Water and 0.015 g of ascorbic acid in 2 g of dist. Water started. After the final temperature (about 100 ° C) was reached, the gel was minced with a meat grinder and dried for 2 h at 150 ° C in a convection oven The dried precursor was coarsely crushed, ground and adjusted to the above particle size distribution.

Use of 0.3% polymerisable surfactant:

Example C

In 966.162 g of an aqueous solution of sodium acrylate with a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 40.2%, 0.590 g Polyethylenglycol300diacrylat (0.15% based on acrylic acid / ester content corresponding to 81%) and 1 , 263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agents. 9.6 g of a 10% strength aqueous solution of the comonomer No. 1 PE 8482 "allyl ether - [(EO) 7- (PO) 3] -H" were then added to this solution, and the monomer solution was stirred in a plastic polymerization vessel for 30 At a temperature of 4 ° C, the polymerization was terminated by the sequential addition of 0.3 g of sodium peroxodisulfate in 10 g of distilled water, 0.07 g of 35% hydrogen peroxide solution in 10 g Distilled water and 0.015 g of ascorbic acid in 2 g of distilled water After the final temperature (about 100 ° C) was reached, the gel was minced with a meat grinder and dried for 2 h at 150 ° C in a convection oven was crushed roughly, ground and adjusted to the above grain distribution.

Use of 0.1% polymerizable surfactant and 0.1% soda slightly

Example D

In 971, 562 g of an aqueous solution of sodium acrylate having a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 40.0%, 0.590 g of polyethylene glycol 300 diacrylate (0.15% based on acrylic acid / ester content corresponding to 81%) and 1.263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agent. 3.2 g of a 10% strength aqueous solution of comonomer No. 1 PE 8482 "allyl ether - [(EO) 7- (PO) 3] -H" were then added to this solution, and the monomer solution was stirred in a plastic polymerization vessel for 30 Purged with nitrogen to remove the dissolved oxygen, at a temperature of 4 ° C., 1 g of finely calcined soda (from Solvay) added and the polymerization by the sequential addition of 0.3 g of sodium peroxodisulfate in 10 g of dist. Water, 0.07 g of 35% hydrogen peroxide solution in 10 g of dist. Water and 0.015 g of ascorbic acid in 2 g of dist. Water started. After the final temperature (about 100 ° C) was reached, the gel was minced with a meat grinder and dried for 2 h at 150 ° C in a convection oven. The dried precursor was coarsely crushed, ground and adjusted to the above particle size distribution.

Use of 0.2% polymerizable surfactant and 0.1% soda slightly

Example E

In 968.362 g of an aqueous solution of sodium acrylate with a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 40.1%, 0.590 g Polyethylenglycol300diacrylat (0.15% based on acrylic acid / ester content corresponding to 81%) and 1 , 263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agents. 6.4 g of a 10% strength aqueous solution of comonomer No. 1 PE 8482 "allyl ether - [(EO) 7- (PO) 3] -H" were then added to this solution, and the monomer solution was stirred in a plastic polymerization vessel for 30 At a temperature of 4 ° C., 1 g of finely calcined soda (from Solvay) was added and the polymerization was initiated by the successive addition of 0.3 g of sodium peroxodisulfate in 10 g of distilled water , 0.07 g of 35% hydrogen peroxide solution in 10 g of distilled water and 0.015 g ascorbic acid in 2 g distilled water.When the final temperature (about 100 ° C) was reached, the gel was minced with a meat grinder and dried 2 h at 150 ° C. in a convection oven The dried precursor was coarsely crushed, ground and adjusted to the above-described particle size distribution.

Use of 0.3% polymerizable surfactant and 0.1% soda slightly

Example F

In 965.162 g of an aqueous solution of sodium acrylate with a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 40.2%, 0.590 g Polyethylenglycol300diacrylat (0.15% based on acrylic acid / ester content corresponding to 81%) and 1 , 263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agents. 9.6 g of a 10% strength aqueous solution of the comonomer No. 1 PE 8482 "allyl ether - [(EO) 7- (PO) 3] -H" were then added to this solution, and the monomer solution was stirred in a plastic polymerization vessel for 30 Rinsed with nitrogen to remove the dissolved oxygen, at a temperature of 4 ° C, 1 g of finely calcined soda (Solvay) was added and polymerization was continued by adding 0.3 g successively Sodium peroxodisulfate in 10 g of dist. Water, 0.07 g of 35% hydrogen peroxide solution in 10 g of dist. Water and 0.015 g ascorbic acid in 2 g dist. Water started. After the final temperature (about 100 ° C) was reached, the gel was minced with a meat grinder and dried for 2 h at 150 ° C in a convection oven. The dried precursor was coarsely crushed, ground and adjusted to the above particle size distribution.

The postcrosslinking of the precursors ("VP") thus obtained was carried out by coating with a solution consisting of ethylene carbonate / water / Al-lactate / Al sulfate in the ratio 1/3 / 0.4 / 0.3% based on 100 g of superabsorbent at 170 ° C for a period of 90 minutes in a drying oven.

The results for Examples 1 A-1 F are summarized in Table 2:

Table 2 PE 8482:

Example Addition Addition CRC CRC FSR OFS AAP SFC 1.5g FHA No.1 Surfactant Soda (VP) (SX) (SX) 0.7psi [units]

Monomer slightly [g / g] [g / g] [g / g / s] [mN / m] [g / g] [g / g]

A 0% 0% 33.7 29.6 0.24 71, 3 26.3 100 25.6

B 0% 0.1% 32.0 28.2 0.29 71, 1 26.1 150 26.1

C 0.3% 0% 34.5 28.9 0.27 66.6 25.2 105 24.2

D 0.1% 0.1% 33.6 29.5 0.35 67.4 25.4 78 25.2

E 0.2% 0.1% 33.8 27.6 0.33 66.5 25.0 131 24.6

F 0.3% 0.1% 33.6 28.5 0.34 65.6 25.3 92 24.8

Example 2

The experimental set-up corresponds to Example 1, which is used as surfactant Blemmer®50PEP-300 "methacrylate ester - [(EO) 3,5- (PO) 2,5] -H", which was previously pre-dissolved in a part of AcS (Examples C. The crosslinking of the precursors thus obtained was carried out by coating with a solution consisting of ethylene carbonate / water / Al-lactate / Al sulfate in the ratio 1/3 / 0.4 / 0, 3% with respect to 100 g of superabsorbent at 170 ° C. over a period of 90 minutes in the drying oven Use of 0.3% polymerisable surfactant:

Example C

In 974.802 g of an aqueous solution of sodium acrylate having a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 39.8% 0.590 g of polyethylene glycol 300 diacrylate (0.15% based on acrylic acid / ester content corresponding to 81%) and 1.263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agents. 0.96 g of the AcS-dissolved comonomer no. 2 Blemmer®50PEP-300 "methacrylate ester- [(EO) 3,5- (PO) 2,5] -H" was then added to this solution, and the monomer solution was dissolved in a plastic Purging the polymerization vessel with nitrogen for 30 minutes to remove the dissolved oxygen At a temperature of 4 ° C., the polymerization was terminated by the successive addition of 0.3 g of sodium peroxodisulfate in 10 g of distilled water, 0.07 g of 35% Hydrogen peroxide solution in 10 g of distilled water and 0.015 g of ascorbic acid in 2 g of distilled water.After the final temperature (about 100 ° C) was reached, the gel was minced with a meat grinder and dried for 2 h at 150 ° C in a convection oven The dried precursor was coarsely crushed, ground and adjusted to the above particle size distribution. Use of 0.1% polymerizable surfactant and 0.1% soda readily

Example D

In 974.442 g of an aqueous solution of sodium acrylate having a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 39.9%, 0.590 g of polyethylene glycol 300 diacrylate (0.15% based on acrylic acid / ester content corresponding to 81%) and 1 , 263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agents. To this solution was then added 0.32 g of AcS pre-dissolved Comonomer No. 2 Blemmer®50PEP-300 "methacrylate ester- [(EO) 3,5- (PO) 2,5] -H" and the monomer solution is dissolved in a plastic Purging the polymerization vessel with nitrogen for 30 minutes to remove the dissolved oxygen At a temperature of 4 ° C., 1 g of finely calcined soda (Solvay) was added and polymerization was initiated by the successive addition of 0.3 g of sodium peroxodisulfate in 10 Water, 0.07 g of 35% strength hydrogen peroxide solution in 10 g of distilled water and 0.015 g of ascorbic acid in 2 g of distilled water were started and after reaching the final temperature (about 100 ° C.), the gel was comminuted with a meat grinder and dried for 2 h in a convection oven at 150 ° C. The dried precursor was coarsely crushed, ground and adjusted to the above-described particle size distribution.

Example E

In 974,122 g of an aqueous solution of sodium acrylate having a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 39.9%, 0.590 g of polyethylene glycol 300 diacrylate (0.15% based on acrylic acid / ester content corresponding to 81%) and 1 , 263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / Ester content corresponding to 76%) as a crosslinker. To this solution was then added 0.64 g of AcS pre-dissolved comonomer # 2 Blemmer®50PEP-300 "methacrylate ester- [(EO) 3,5- (PO) 2,5] -H" and the monomer solution is dissolved in a plastic Purging the polymerization vessel with nitrogen for 30 minutes to remove the dissolved oxygen At a temperature of 4 ° C., 1 g of finely calcined soda (Solvay) was added and polymerization was initiated by the successive addition of 0.3 g of sodium peroxodisulfate in 10 Water, 0.07 g of 35% strength hydrogen peroxide solution in 10 g of distilled water and 0.015 g of ascorbic acid in 2 g of distilled water were started and after reaching the final temperature (about 100 ° C.), the gel was comminuted with a meat grinder and dried for 2 h in a convection oven at 150 ° C. The dried precursor was coarsely crushed, ground and adjusted to the above-described particle size distribution.

Example F

In 973.802 g of an aqueous solution of sodium acrylate having a degree of neutralization of 70 mol% (based on acrylic acid) and a total monomer concentration of 39.9%, 0.590 g of polyethylene glycol 300 diacrylate (0.15% based on acrylic acid / ester content corresponding to 81%) and 1 , 263 g of polyethylene glycol (440) monoallyl ether acrylate (0.30% based on acrylic acid / ester content corresponding to 76%) were dissolved as crosslinking agents. 0.96 g of the AcS-dissolved comonomer no. 2 Blemmer®50PEP-300 "methacrylate ester- [(EO) 3,5- (PO) 2,5] -H" was then added to this solution, and the monomer solution was dissolved in a plastic Purging the polymerization vessel with nitrogen for 30 minutes to remove the dissolved oxygen At a temperature of 4 ° C., 1 g of finely calcined soda (Solvay) was added and polymerization was initiated by the successive addition of 0.3 g of sodium peroxodisulfate in 10 water, 0.07 g of 35% strength hydrogen peroxide solution in 10 g of distilled water and 0.015 g of ascorbic acid in 2 g of distilled water were started After the final temperature (about 100 ° C) was reached, the gel was comminuted with a Meat mincer and dried for 2 h in a convection oven at 150 ° C. The dried precursor was coarsely crushed, ground and adjusted to the above-described particle size distribution The results for Examples 2A-F are summarized in Table 3:

Table 3 Blemmer®50PEP-300 Example Addition Addition CRC CRC FSR OFS AAP SFC 1.5g FHA # 2 Surfactant Soda (VP) (SX) (SX) 0.7psi [units]

Monomer slightly [g / g] [g / g] [g / g / s] [mN / m] [g / g] [g / g]

A 0% 0% 33.7 29.6 0.24 71, 3 26.3 100 25.6

B 0% 0.1% 32.0 28.2 0.29 71, 1 26.1 150 26.1

C 0.3% 0% 31, 8 26.8 0.24 67.5 24.5 189 22.5

D 0.1% 0.1% 32.9 27.8 0.34 68.5 25.1 113 25.1

E 0.2% 0.1% 32.2 26.6 0.30 67.8 24.9 125 23.8

F 0.3% 0.1% 31, 8 26.6 0.31 67.9 25.1 144 22.9

Example 3

The experimental setup corresponds to Example 2 except that the surfactant Blemmer®55PET-800 "methacrylate ester - [(EO) 10- (BO) 5] -H" is used the coating with a solution consisting of ethylene carbonate / water / Al-lactate / Al sulfate in the ratio 1/3 / 0.4 / 0.3%, based on 100 g of superabsorbent at 170 ° C over a period of 90min.

The results for the examples of 3 are summarized in Table 4:

Table 4 Blemmer®55PET-800

Beispiet Supplement Addition CRC CRC FSR OFS AAP SFC 1.5g FHA

No. 3 Surfactant Soda (VP) (SX) (SX) 0.7psi [units]

Monomer slightly [g / g] [g / g] [g / g / s] [mN / m] [g / g] [g / g]

A 0% 0% 33.7 29.6 0.24 71, 3 26.3 100 25.6

B 0% 0.1% 32.0 28.2 0.29 71, 1 26.1 150 26.1

E 0.2% 0.1% 32.5 27.5 0.32 57.6 26.0 85 23.2

Example 4

The experimental set-up corresponds to Example 2, which is used only as a surfactant Blemmer®70PEP-350B "Methacrylate ester- [EO] 5- [PO] 2-H." The amounts of the surfactant used varied The post-crosslinking of the precursors thus obtained was carried out by the coating with a solution consisting of ethylene carbonate / water / Al-lactate / Al sulfate in a ratio of 1/3 / 0.4 / 0.3% based on 100 g of superabsorbent at 170 ° C. over a period of 90 minutes in a drying oven. The results for Examples 4A-F are summarized in Table 5: TABLE 5 Blemmer®70PEP-350B

Example Addition Addition CRC CRC FSR OFS AAP SFC 1.5g FHA # 4 Surfactant Soda (VP) (SX) (SX) 0.7psi [units]

Monomer slightly [g / g] [g / g] [g / g / s] [mN / m] [g / g] [g / g]

A 0% 0% 33.7 29.6 0.24 71, 3 26.3 100 25.6

B 0% 0.1% 32.0 28.2 0.29 71, 1 26.1 150 26.1

C 0.3% 0% 31, 2 27.1 0.26 68.5 25.4 161 24.1

D 0.1% 0.1% 32.3 27 0.32 70.1 26.3 104 25.1

E 0.2% 0.1% 32.7 27.3 0.33 68.6 25.7 134 24.8

F 0.3% 0.1% 32.1 27.1 0.33 68.3 25.2 150 25.0

Example 5 (Comparative Example)

The experimental setup corresponds to Example 1 except that sodium lauryl ether sulfate (Hansa-Group AG, Duisburg) was used as the surfactant. NaLES is not a copolymerizable surfactant. The amounts of surfactant and carbonate used varied. The surface postcrosslinking of the precursors thus obtained is carried out by coating with a solution consisting of ethylene carbonate / water / Al-lactate / Al sulfate in the ratio 1/3 / 0.4 / 0.3% rel. to 100g precursor and subsequent heating at 170 ° C over a period of 90min. in the drying cabinet. The results for Examples 5B-5D are summarized in Table 6:

Table 6 Sodium lauryl ether sulfate

Example Addition Addition CRC CRC FSR OFS AAP SFC FHA

No. 5 Surfactant Soda VP (SX) (SX) [mN / OJpsi 1.5g

Monomer light [g / g] [g / g] [g / g / s] m] [g / g] [units] [g / g]

A 0% 0% 33.7 29.6 0.24 71, 3 26.3 100 25.6

B 0% 0.2% 31, 5 ** 28.3 0.46 68.6 25.7 83 23.3

C 0.3% 0% 31, 6 * 28.3 0.42 38.0 24.9 68 16.2

D 0.3% 0.2% 32.8 ** 28.2 0.57 37.5 25.2 62 16.3

* Crosslinking PEG300DA / PEGMAE-A: 0.2% / 0.4% rel. on acrylic acid

** Crosslinking PEG300DA / PEGMAE-A: 0, 18% / 0.36% rel. on acrylic acid

The non-copolymerizable surfactant showed a significant deterioration in the FHA value.

The OFS values of the water-absorbing polymers according to the examples of the invention described above are above 50 mN / m, preferably above 55 mN / m, especially preferably above 60 mN / m, and most preferably above 62 mN / m. The OFS value must not exceed a value of 72 mN / m. Advantageously, this minimizes the rewet value (eg, backsheet rewet) in the diapers and maintains the capillarity of the superabsorber in the absorbent core of the diaper, which thus corresponds to high FHA values. The use of copolymerizable surface-active comonomers avoids a great reduction of the OFS values.

Advantageously, the simultaneous use of the surfactant comonomers and carbonate results in a synergistic increase in the levels of FSR and FHA. According to the invention, in particular, the aforementioned effect is exhibited in the case of water-absorbing polymers which have an OFS value greater than 60. The water-absorbing polymers according to the invention additionally show good parameter properties with regard to the CRC, SFC, and AAP values.

According to the following table, it was shown that according to the invention incorporation of the copolymerizable surfactants ("surfactant monomers", SM) into the network of the hydrogel polymer took place The extractables are shown in the last column of the table In accordance with the invention, less than 8% of extractable surfactants / surfactant monomers were detected in principle, demonstrating that the surfactant was incorporated into the polymer matrix of the superabsorber.

Example Extractable% based on the polyether No. of polyether content (ppm) used

1A <10 <0.4%

1 C 69 2.8%

1 F 172 7.0%

2C <10 <0.4%

2F <10 <0.4%

3C 14 0.6%

3F 18 0.7%

4C <10 <0.4%

4F <10 <0.4%

Claims

claims

A process for producing a water-absorbent polymer composition comprising the process steps

(i) mixing

(a1) 0.1 to 99.999% by weight, preferably 20 to 98.99% by weight and particularly preferably 30 to 98.95% by weight of polymerisable, ethylenically unsaturated,

acid group-containing monomers or their salts or polymerizable, ethylenically unsaturated, a protonated or quaternized nitrogen

containing monomers, or mixtures thereof, wherein at least ethylenically unsaturated, acid group-containing monomers, preferably acrylic acid-containing mixtures are particularly preferred,

(a4) 0 to 30 wt .-%, preferably 1 to 20 wt .-% and particularly preferably 5 to 10 wt .-% of water-soluble polymers, and

(a5) 0 to 20 wt .-%, preferably 0.01 to 7 wt .-% and particularly preferably 0.05 to 5 wt .-% of one or more auxiliaries, wherein the sum of the amounts by weight (a1) to (a5) 100% by weight,

(ii) radical polymerization with crosslinking to give a water-insoluble,

to form aqueous untreated hydrogel polymer,

(iii) drying the hydrogel polymer,

(iv) grinding and screening the hydrogel polymer,

(V) surface postcrosslinking of the ground and sieved hydrogel polymer and

(vi) drying and packaging of the water-absorbing polymer, wherein

the aqueous monomer solution, before the addition of the initiator and the start of the radical polymerization, 0.01 to 5 wt .-%, preferably 0.02 to 2 wt .-% and particularly preferably 0.07 to 1 wt .-% of at least one Surfactants from the group of nonionic unsaturated polyether copolymers and optionally 0.01 to 5 wt .-%, preferably 0.02 to 2 wt.% And particularly preferably 0.07 to 1 wt .-% of a blowing agent having a particle size of 10 μηη be added to 900μηι, based on the water-absorbing polymer. A process for producing a hydrogel polymer comprising the process steps

(i) mixing

(ii) free radical polymerization with crosslinking to form a water insoluble, aqueous untreated hydrogel polymer,

(iii) drying the hydrogel polymer,

(iv) grinding and screening the hydrogel polymer,

in which

the aqueous monomer solution, before the addition of the initiator and the start of the radical polymerization, 0.01 to 5 wt .-%, preferably 0.02 to 2 wt .-% and particularly preferably 0.07 to 1 wt .-% of at least one Surfactants from the group of nonionic unsaturated polyether copolymers and optionally 0.01 to 5 wt .-%, preferably 0.02 to 2 wt.% And particularly preferably 0.07 to 1 wt .-% of a blowing agent having a particle size of 10 μηη be added to 900μηι, based on the hydrogel polymers.

A method according to claim 1 or 2, characterized in that the aqueous monomer solution at least one surfactant from the group of non-ionic unsaturated polyether copolymers and 0.01 to 5 wt .-%, blowing agent with a Particle size of 10 μηι to 900 μηι be added, based on the water-absorbing polymer.

Method according to one of the preceding claims, characterized in that

the surfactant is composed of at least one ethylene glycol unit and of at least one further alkylene glycol unit having 3 to 6 C atoms different from the ethylene glycol unit.

Method according to one of the preceding claims, characterized in that the surfactant from at least one ethylene glycol unit and at least one further unit from the group of propylene glycol or butylene glycol, constructed.

Method according to one of the preceding claims, characterized in that the unsaturated polymerizable surfactant at least one terminal functionalities from the group of vinyl ether, (meth) allyl ether, 4-vinylbenzyl ether, (meth) acrylamide, methacrylic ester or Contains acrylic ester group.

Method according to one of the preceding claims, characterized in that the unsaturated polymerizable surfactants at least one terminal functionality from the group of vinyl ether, (meth) allyl ether, 4-vinylbenzyl ether, (meth) acrylamide, methacrylic ester or Acrylic ester group and a non-polymerizable end-group functionality selected from the group of hydroxyl, hydroxyl group which may be etherified with a radical R or esterified with a radical 0 = CR.

Method according to one of the preceding claims, characterized in that the radical R is selected from the group of linear or branched to C _1Q- alkyl radicals, preferably C ₂ - to C ₇ _Alkylreste, more preferably C _{3 to} C ₄ - alkyl radicals or a C ₆ to C, preferably C ₆ to C ₉ alkylaryl group.

9. The method according to any one of the preceding claims, characterized in that the unsaturated polyether surfactant is a compound of the following formula:

wherein the alkylene glycol units (C ₂ H ₄ O) and (C _q H _2q O) are random, block or gradient distributed, -H or -CH 3 R 2 is a carbonyl group (C = O) and R 1 is -H, linear or branched C | | - to cy-alkyls, Cg- to Cg-alkylaryls or C- | - to Cy-acyl radicals, q is a number from 3 to 4, n and m is a number from 1 to 20, preferably 2 to 12, particularly preferably 4 to 8.

10. The method according to any one of the preceding claims, characterized in that the unsaturated polyether surfactant, a compound of the following formula:

wherein the alkylene glycol units (C ₂ H ₄ O) and (C _q H _2q O) are randomly or as a gradient, R 1 is -H or -CH 3, R 1 is an alkylene group from the group of methylene or ethylene, and R 3 is H, linear or branched C | - to cy-alkyls, Cg- to Cg-alkyl-aryls or C- | - to Cy acyl radicals, q is a number from 3 to 4, n and m is a number from 1 to 20, preferably 2 to 12, particularly preferably 4 to 8.

1 1. Method according to one of the preceding claims, characterized in that the surfactant and the blowing agent are added together to the monomer solution.

12. The method according to any one of the preceding claims, characterized in that the blowing means consist of a powder of inorganic particles.

13. The method according to any one of the preceding claims, characterized in that the blowing agent consist of soda particles.

14. The method according to any one of the preceding claims, characterized in that the blowing agent has a preferred particle size of 10 μηη to 900 μηη, preferably 50 μηη to 500 μηη and more preferably 100 μηη to 450 μηι, has.

15. The method according to any one of the preceding claims, characterized in that more than 35 wt .-% of the blowing agents have a particle size of 100-300μηι.

16. The method according to any one of the preceding claims, characterized in that the FSR in the range of 0.30 to 0.70 is preferably from 0.35 to 0.60, particularly preferably from 0.40 to 0.50.

17. The method according to any one of the preceding claims, characterized in that the surface tension (OFS) in the range of about 50 mN / m, preferably above 55 mN / m, more preferably above 60 mN / m and most preferably above 65 mN / m is

18. The method according to any one of the preceding claims, characterized in that the permeability as SFC (1, 5g) in the range of 30 to 200, preferably 50 to 180, particularly preferably from 70 to 150.

19. A water-absorbing polymer obtainable according to any one of claims 1 to 18.

20. composite comprising a water-absorbing polymer according to one of the preceding claims.

21. A process for preparing a composite, wherein a water-absorbent polymer according to any one of the preceding claims and an adjuvant are brought into contact with each other.

22. Composite, obtainable by a process according to claim 21.

23. Foams, shaped articles, fibers, films, cables, sealing materials, liquid-absorbent hygiene articles, carriers for plant and fungi growth-regulating agents, packaging materials, floor additives or building materials, comprising the water-absorbing polymer according to one of claims 1 to 19 or the composite according to claim 20 or 22.

24. The use of the water-absorbing polymer according to any one of claims 1 to 19 or a composite containing a water-absorbing polymer according to any one of claims 20 or 22 in foams, moldings, fibers, films, films, cables, sealing materials, liquid-absorbent hygiene articles, supports for plant and fungi growth regulating agents, packaging materials, sediment additives, for the controlled release of active substances or in building materials.